000			02748ntm a2200349 i 4500
003			MY-KuUP
005			20260611093216.0
006			t||||fr|||| 000 0
007			ta
008			260611t20242024my a|||fr|||| 000 0 eng d
020			_aTHE0010585 (Local) _qHardback
040			_aUMPSA _beng _cUMPSA _erda
090			_aFTKKP .A43 2024 r Bc.
100	1		_aAlden Michael Sta Maria, _eauthor.
245	1	0	_aProduction of bio-gasoline from cracking reaction of waste cooking oil using waste concrete as the catalyst / _cAlden Michael Sta Maria
264		1	_aKuantan, Pahang : _bUMPSA, _c2024
264		4	_c© 2024
300			_a51 pages : _billustrations ;
336			_2rdacontent _atext
337			_2rdamedia _aunmediated
338			_2rdacarrier _avolume
347			_2rda _atext file _bPDF
500			_aFaculty of Chemical and Process Engineering Technology
502			_aFinal Year Report (Bachelor of Chemical Engineering Technology) -- Universiti Malaysia Pahang Al-Sultan Abdullah - 2024
504			_aInclude bibliographical reference
520	3		_aThe growing need for sustainable and environmentally friendly energy sources has sparked discussions on finding alternatives to conventional fossil fuels due to the negative impacts that fossil fuels pose on the environment. Bio-gasoline, a renewable biofuel, can be produced from waste cooking oil (WCO) and has emerged as a potential substitute to fossil fuels. The production of bio-gasoline falls in the range of C5–C12 hydrocarbons. This study explores the potential of waste concrete as a catalyst to produce bio-gasoline through catalytic cracking of WCO. The study focused on exploring the impacts of catalyst loading and particle size on the yield and selectivity of C5-C12 hydrocarbons obtained from WCO using three different catalyst loadings ranging from 5g to 10g as well as three different particle sizes of ranging from 75 to 600 μm at a fixed temperature of 400 ºC. The research findings highlighted that for different catalyst loading, the highest yield and selectivity of C5-C12 hydrocarbons were achieved using 10g of calcined concrete catalyst (59.14%, 1.45), while at different catalyst particle size, the highest yield and selectivity was obtained using 75 - 150 μm of calcined concrete catalyst (46.56%, 0.87). The results suggest that a higher catalyst loading, and smaller particle size will increase the yield and selectivity of C5-C12 hydrocarbons obtained during the catalytic cracking of WCO.
610	2	0	_aFaculty of Chemical and Process Engineering Technology _xDissertations
650		0	_aUniversities and colleges _xDissertations
650		0	_aTheses _xDissertations
856			_uhttps://umpir.ump.edu.my/id/eprint/46923
942			_2lcc _cPSM
999			_c104973 _d104979